Products

Braskem HDPE 5040

    • Product Name: Braskem HDPE 5040
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
    • CONTACT NOW
    Specifications
    HS Code 971316
    Polymertype High Density Polyethylene
    Density 0.950 g/cm³
    Meltflowrate 4.0 g/10 min at 190°C/2.16 kg
    Tensilestrengthatyield 24 MPa
    Tensilestrengthatbreak 24 MPa
    Elongationatbreak 1000%
    Flexuralmodulus 1100 MPa
    Notchedizodimpactat23c 80 J/m
    Vicatsofteningtemperature 125°C
    Heatdeflectiontemperatureat0 45mpa 75°C
    Shoredhardness 65
    Environmentalstresscrackresistance >1000 h
    Moldshrinkage 0.020 in/in

    As an accredited Braskem HDPE 5040 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Braskem HDPE 5040 comes in 25 kg polyethylene-lined paper bags, palletized at 1,000 kg per shrink-wrapped pallet.
    Container Loading (20′ FCL) 20′ FCL container loading of Braskem HDPE 5040 resin in 25 kg bags, palletized, shrink-wrapped, and secured for ocean transport.
    Shipping Braskem HDPE 5040 is shipped as non-hazardous polyethylene pellets in 25 kg bags, 1,000–1,250 kg big bags, octabins, or bulk trucks/railcars. Keep containers dry, clean, and sealed, away from heat, sunlight, moisture, and contamination. Store cool and follow local transport and supplier instructions.
    Storage Store Braskem HDPE 5040 in a cool, dry, well-ventilated area away from direct sunlight, heat, ignition sources, and strong oxidizers. Keep in original sealed bags or containers, on pallets off the floor, to prevent moisture, dust, and contamination. Avoid excessive stacking. Use first-in, first-out. Maintain ambient temperature and keep away from odorous materials.
    Shelf Life Braskem HDPE 5040 has a two-year shelf life when stored in original packaging, cool, dry, and away from direct sunlight.
    Application of Braskem HDPE 5040

    Braskem HDPE 5040 Application-Specific Processing, Compliance, and Formulation Data

    Extrusion Blow Moulding Conditions for UN-Certified Intermediate Bulk Packagings

    Braskem HDPE 5040 is converted on accumulator-head blow moulding platforms into closed-head 1H1 drums and open-head 1H2 containers used for dangerous-goods logistics. Incoming resin control under ASTM D1238 at 190 °C/2.16 kg and density verification under ISO 1183-1 is maintained because lot-level traceability is audited against the UN Model Regulations Chapter 6.1 and, for US-bound packagings, 49 CFR Part 178. At the die head a melt temperature of 180–220 °C is held, with accumulator head dwell times adjusted so that parison sag remains below 15% of programmed length over a 2.0–6.0 s hang time. Formulation for outdoor-stored industrial containers typically includes a UV-stabilized carbon black masterbatch at 2.0–4.0 wt% and, where solvent-based filling lines create ignition risk, an antistatic conductive carbon black masterbatch at 1.0–3.0 wt%. Closed-loop regrind from pinch-off flash is incorporated at up to 25 wt% for UN-certified packs and up to 40 wt% for non-hazardous industrial containers, provided the regrind is dried to below 0.05% moisture and melt-filtered through a 40–80 mesh screen pack. Production tools use single-screw extruders of 24:1–30:1 L/D with barrier screws and grooved feed sections; clamping force for 220 L tooling ranges from 1,200–2,000 kN, blow air pressure is set between 0.6–0.8 MPa, and mould coolant is controlled at 10–30 °C. Cycle time for 120 L drums is typically 120–180 s, with the pinch-off weld line mechanically inspected for thickness reduction below 25% of the nominal wall section because this zone is the primary drop-test failure origin. Terminal pack types include 30 L 3H1 jerricans, 60 L open-head drums, 120 L closed-head drums, and 220 L closed-head drums used for lubricants, water-based adhesives, solvent-based metalworking fluids, and low-viscosity paste intermediates.

    Test requirementReference clauseVerification condition
    Drop testUN 6.1.5.3 / 49 CFR 178.603Drop height 1.2 m for Packing Group II at 23 °C and −18 °C; no leakage from closure or drum body
    LeakproofnessUN 6.1.5.4 / 49 CFR 178.604Internal air pressure 20 kPa for 5 min under water; no bubble evolution
    Hydrostatic pressureUN 6.1.5.5 / 49 CFR 178.605Gauge pressure 100 kPa held for 30 min; no cracking or leakage
    StackingUN 6.1.5.6 / 49 CFR 178.606Load equal to 1.8 m stack at 40 °C for 28 days; no instability or deformation causing stacking failure

    Inline fluorination of mono-layer Braskem HDPE 5040 jerrican interiors modifies the inner 5–50 nm surface region, replacing C–H bonds with C–F bonds and reducing the steady-state permeation of aliphatic hydrocarbons by 10–100× relative to untreated HDPE. This approach is applied to crop protection liquid packaging rather than coextruded barrier structures where seam integrity and recycled-content economics prohibit multilayer tooling. The relevant compliance base includes the US EPA container and containment rules under 40 CFR Part 165, the CLP Regulation (EC) 1272/2008 for classification and labelling, and FAO/WHO guidelines for pesticide packaging handling when export cargo is destined for smallholder agricultural programmes. Typical dry-blend formulation retains 2.5–3.5 wt% of a UV-stabilized carbon black masterbatch to reduce embrittlement during outdoor warehouse block stacking; a low-volatility PE wax processing aid is added at 0.05–0.15 wt% only when high-speed trimming generates surface melt fracture on older blow moulder slots. Inline fluorination is conducted by injecting a pre-mixed gas stream of 0.1–0.3 % fluorine in nitrogen into the parison internal cavity for 0.5–3.0 s after blowing pressure begins to expand the part, with excess gas scrubbed in an alkaline media bed before atmospheric release. The extrusion blow moulding platform operates at 190–220 °C melt temperature inside an enclosed cell with continuous F₂ detection at 0.1 ppm alarm threshold. Wall thickness programming must maintain corner sections above 2.0 mm because fluorination does not compensate for mechanical thinning at pinch-off seams. Permeation performance is verified under ASTM D2684 using n-decane or xylene simulant at 40 °C over 28 days, and container burst validation is run at 1.5× the labelled relief pressure. Finished forms include 1 L, 5 L, and 20 L mono-layer jerricans for emulsifiable concentrates, soluble liquid herbicides, systemic fungicides, and adjuvant-surfactant premixes.

    How Thermal Cycling Under Bonnet Conditions Constrains Coolant Reservoir Wall Thickness?

    Accumulator-head machines running Braskem HDPE 5040 for automotive washer fluid reservoirs and coolant expansion bottles operate under a narrower control band than industrial drums because the part must survive −40 °C cold-soak followed by 120 °C coolant circulation without panel deformation. The governing specification is usually derived from ISO 16750-4 environmental loading tests and OEM-specific pressure-cycling protocols that subject the component to 0–1.2 bar internal pressure sweeps for 5,000–200,000 cycles at 80 °C coolant temperature. Formulation in under-hood applications uses carbon black masterbatch at 2.0–3.0 wt% for UV blocking in semi-translucent reservoir areas exposed to sunlight through cowl louvers, and a hindered phenolic/phosphite thermal stabilizer package at 0.20–0.50 phr to limit melt-flow drift during long accumulator hold times at 200–220 °C. No migratory plasticizer is permitted because windshield washer alcohols can extract low-molecular-weight additives and deposit them on glass through nozzle misting. The extrusion head tooling is programmed to produce a wall-thickness distribution between 2.2 mm and 3.5 mm in the main shell, with minimum thickness at pinch seams set to 2.5 mm to resist stress cracking from ethylene glycol/borate inhibitor chemistries. Clamp force for 2–6 L reservoirs is typically 500–800 kN, and blow mould cooling water is held at 10–20 °C to minimize post-mould shrinkage before robot trimming. Mounting features are either blow-moulded-in inserts or hot-plate-welded injection-moulded sockets, and each weld line is subjected to 0.5 MPa burst testing followed by leak tester evacuation at −20 kPa for 10 s. Finished parts include 2–7 L windshield washer reservoirs, 1–4 L coolant expansion bottles, and 15–25 L heavy-duty truck reservoirs that integrate level-sensor bosses and filler-neck trims.

    When Bleach-Containing Household Cleaners Force ESCR Screening Before Tool Design

    Concentrated alkaline household cleaners and liquid laundry detergents generate stress-cracking conditions in high-density polyethylene bottles because the bottle wall is simultaneously subjected to internal headspace pressure, squeeze forces at the handle, and polar surfactant attack at the outer surface. Braskem HDPE 5040 is converted into these packages on reciprocating-screw blow moulders with 6–12 parison heads; melt temperature is maintained at 190–215 °C, and chilled mould water at 10–15 °C keeps cycle times between 8–20 s for 500 mL bottles. Compliance for this segment follows FDA 21 CFR 177.1520 when the container is intended for food contact or dual-use household storage, and EU Regulation (EU) No 10/2011 for migration limits when exports enter the European Economic Area; REACH Annex XVII restrictions are screened before tinting masterbatch selection. The formulation addition ratio is comparatively low: color concentrate at 1.0–3.0 wt%, white pearlescent masterbatch at 2.0–4.0 wt% for opaque laundry lines, and slip/antiblock concentrate at 0.5–1.0 wt% only where label application requires consistent coefficient of friction. ESCR validation is run under ASTM D1693 Condition B with 10% nonylphenoxy poly(ethyleneoxy) ethanol at 50 °C, and a production-lot F50 value below 48 h triggers quarantine because field failures in alkaline bleach formulations are observed at handle weld lines, not in the flat sidewall. Post-mould leak testing applies 10 kPa differential pressure for 3–5 s in multi-cavity conveyor systems, and top-load testing follows ASTM D2659 at 23 °C and 60% RH to a target deformation below 6 mm. Finished package types include 250 mL trigger-spray cleaner bottles, 1 L bleach-containing household cleaners, 3–5 L laundry detergent bottles with integrated handles, and 100–300 mL personal care containers for lotions and body washes.

    Conversion of Braskem HDPE 5040 into clinical-waste containment packages requires thick-walled extrusion blow moulding to achieve puncture resistance and retained integrity after multiple handling cycles. The regulatory framework for this segment includes UN 3291 for regulated medical waste when transport is placed under the Dangerous Goods Regulations, the European ADR packing instruction P621/P622 for infectious substances or clinical waste, and ISO 23907-1:2019 sharps-injury protection requirements for container leakage, puncture, and impact. Formulation additions are restrained to a carbon black masterbatch at 2.0–3.0 wt% for opacity and UV screening, with no post-consumer resin allowed in sharps containers because ISO puncture-test repeatability is compromised by variable regrind contamination; clean in-house regrind may be added up to 15 wt% only after melt filtration through a 60 mesh screen and documented batch segregation. Processing uses an accumulator-head blow moulding line with a 24:1 L/D low-shear screw, melt temperature 185–205 °C, and blow pressure 0.5–0.7 MPa; wall thickness is programmed to 2.5–5.0 mm depending on container volume, and the mould closing speed is reduced in the final 20 mm of stroke to avoid impact cracks at the pinch seam. Drop testing is performed at 0.8 m on to a concrete floor at 23 °C and −10 °C with no leakage or wall perforation; needle penetration testing under ISO 23907-1 may require a minimum wall thickness of 2.5 mm at the sidewall and 3.0 mm at the base corner. Terminal products include 0.5 L countertop sharps collectors, 6–12 L wall-mounted sharps containers, 20–35 L clinical-waste pails for autoclave treatment, and satellite accumulation containers used in hospital laboratory zones.

    Free Quote

    Competitive Braskem HDPE 5040 prices that fit your budget—flexible terms and customized quotes for every order.

    For samples, pricing, or more information, please contact us at +8618136850665 or mail to admin@ascent-chem.com.

    We will respond to you as soon as possible.

    Tel: +8618136850665

    Email: admin@ascent-chem.com

    Inquiry

    Get Free Quote of Ascent Petrochem Holdings Co., Limited

    Flexible payment, competitive price, premium service - Inquire now!

    Certification & Compliance
    More Introduction

    For injection molding operations requiring a medium-flow high-density polyethylene with density above 0.950 g/cm³, Braskem HDPE 5040 is supplied as a pelletized resin intended for rigid packaging, closures, caps, and thin-wall containers. The grade is differentiated from fractional-melt HDPE by its melt flow rate of 4.0 g/10 min under ASTM D1238 at 190°C/2.16 kg and from lower-density HDPE by its nominal density of 0.954 g/cm³ under ASTM D792.

    These two values establish the basic processing classification: the 4.0 g/10 min flow rate is high enough to fill thin sections and fine threads on standard hydraulic injection molding machines, while the density remains within the range associated with high stiffness and top-load resistance. The resin is not intended for extrusion blow molding or film because its melt strength is lower than that of fractional-melt grades. Instead, the narrow molecular weight distribution is designed to reduce cycle time and improve dimensional stability in injection-molded parts.

    Typical property framework for Braskem HDPE 5040
    PropertyTest methodExpected range or typical value
    DensityASTM D7920.954 g/cm³
    Melt flow rate, 190°C/2.16 kgASTM D12384.0 g/10 min
    Tensile yield strengthASTM D63824–28 MPa (lot-dependent)
    Flexural modulusASTM D7901,000–1,200 MPa
    Notched Izod impact, 23°CASTM D2563.0–5.0 kJ/m²
    Vicat softening pointASTM D1525120–128°C
    Shore D hardnessASTM D224060–64

    The mechanical ranges in the table are not specification limits; they are provided to support preliminary material selection. Current supplier datasheet values should be used for final mold design and part qualification because polyolefin mechanical data are test-specimen-dependent and lot-dependent.

    How does the melt-flow ratio affect injection-molding performance relative to fractional-melt HDPE?

    The flow classification of Braskem HDPE 5040 is defined by the 4.0 g/10 min melt flow rate; typical blow-molding and film HDPE grades exhibit melt flow rates below 1.0 g/10 min and often below 0.2 g/10 min. In a reciprocating-screw injection molding machine, this difference reduces the injection-pressure requirement for a given wall thickness and shortens the residence time necessary to reach uniform melt temperature. The trade-off is a reduction in environmental stress crack resistance, as measured by ASTM D1693, because ESCR declines as molecular weight and melt viscosity decrease. For containers holding aggressive liquids or subjected to flexural fatigue, this boundary must be evaluated against the end-use requirement.

    Compared with high-flow thin-wall molding grades with melt flow rates above 20 g/10 min, Braskem HDPE 5040 retains higher tensile strength and low-temperature impact resistance. The density of 0.954 g/cm³ also places it above high-flow low-density or medium-density grades in terms of top-load strength. However, in wall sections below 0.8 mm, the higher viscosity of HDPE 5040 may require higher injection velocities or elevated melt temperatures near the upper limit of the processing window.

    The molecular weight distribution is narrow enough to allow clean cavity filling without excessive differential shrinkage, but the grade is not a low-warpage specialty resin. Part geometry, gate location, and mold temperature uniformity remain the dominant variables. On multi-cavity closures, hot-runner flow balance within 2% across cavities is recommended to prevent short shots and dimensional scatter.

    Thermal and rheological constraints during high-speed injection molding

    On injection molding machines with screw L/D ratios between 20:1 and 25:1, the recommended melt-temperature window at the nozzle is 180°C to 220°C. At temperatures below 180°C, residual unmelt can produce weld-line weakness and thread deformation in closures. At temperatures above 220°C, thermal oxidative degradation may shift viscosity, create yellowing, and reduce notched Izod impact. Shear heating in gates with diameters below 1.0 mm can raise local melt temperature by 10–30°C; therefore, nozzle temperature should not be used as the sole indicator of average melt temperature.

    Mold temperature should be maintained between 20°C and 40°C. The lower boundary accelerates skin solidification and reduces cycle time but increases frozen-in stress and warpage risk in thick sections. The upper boundary improves surface gloss and weld-line strength but increases cooling time. A cavity-to-cavity mold temperature differential above ±5°C can produce measurable differential shrinkage in flat parts, causing warpage that is frequently misread as a material defect. At mold temperatures below 20°C, premature gate freeze-off can prevent adequate packing and produce sink marks in ribs and bosses.

    The resin does not require desiccant drying under normal dry storage conditions. If surface condensation forms after cold storage or high humidity, drying for 2 h at 80°C is sufficient; higher drying temperatures may lead to pellet agglomeration in the hopper. The polymer is non-hygroscopic, so moisture-related processing problems are usually caused by surface moisture or contaminated regrind rather than absorbed water.

    On machines with worn check rings, melt flow rate can appear to drift between shots. The resulting short shot or flash is often incorrectly attributed to resin lot changes. A check-ring leakage test should be performed before adjusting material parameters. Screw retraction speed, decompression, and back pressure should be set to avoid air entrapment and melt decompression in the cushion. Cushion length of 3–5 mm is typical for closures.

    Processing start parameters for Braskem HDPE 5040
    ParameterRecommended start point
    Melt temperature, nozzle180–220°C
    Mold temperature20–40°C
    Predrying if condensation80°C for 2 h
    Screw L/D ratio20:1–25:1
    Back pressure, if regrind mixing is required0.5–1.0 MPa

    Injection velocity and hold pressure are part-specific. The processing window is not a single fixed setpoint; it is a matrix bounded by melt temperature, mold temperature, gate design, and part wall thickness. When thin-wall parts are molded at high speed, the shear rate at the gate can exceed 1,000 s⁻¹. Under those conditions, viscous heating lowers apparent viscosity and may permit filling at lower nozzle temperatures, but the actual melt temperature entering the cavity must still remain below 230°C to avoid degradation.

    In caps and closures with wall thickness below 1.5 mm, the combination of 4.0 g/10 min flow and density 0.954 g/cm³ allows adequate filling of fine thread details without excessive injection pressure. Top-load strength of finished closures is influenced by thread geometry and sidewall taper more than by material alone; validation should use a calibrated universal testing machine with compression platen speed controlled to the producer’s test specification. Published data for this specific configuration is limited.

    In thin-walled housewares and rigid containers, molded part mass can be reduced without losing short-term stiffness relative to lower-density polyethylene grades. However, continuous load-bearing performance at temperatures above 60°C should be validated against creep rupture data under ISO 899 or equivalent; HDPE undergoes time-dependent deformation under sustained load, and the higher density does not eliminate creep.

    In industrial pails and crates, impact performance depends on wall thickness, corner radius, and processing history. Notched Izod impact values in the 3.0–5.0 kJ/m² range under ASTM D256 are indicative, but finished parts in instrumented drop tests may fail in ductile or brittle modes depending on orientation and stress concentration.

    When Braskem HDPE 5040 replaces a fractional-melt blow-molding grade in rigid packaging

    When a processor substitutes a fractional-melt HDPE with Braskem HDPE 5040 to gain injection-molding productivity, the lower molecular weight reduces melt strength and ESCR. This substitution is acceptable only for non-pressurized, non-aggressive applications where the original ESCR margin was not fully utilized. For detergent bottles, chemical containers, or fuel-contact articles, the lower ESCR may be a disqualifying factor under ASTM D1693 or ASTM D256.

    The density of 0.954 g/cm³ provides higher top-load strength than blow-molding HDPE with density near 0.950 g/cm³, but the difference is approximately linear with density and not a substitute for structural ribbing. Dimensional stability is generally improved due to the injection-molded part design rather than an intrinsic polymer property.

    Colorability and additive compatibility are similar to other HDPE grades. Avoid contamination with polypropylene or PVC; melt blending with polypropylene can create phase-separated domains that reduce impact strength and create surface defects. Avoid amine-based additives that may cause discoloration or interfere with organoleptic requirements in food-contact applications.

    For food-contact applications, the final article must comply with 21 CFR 177.1520 for olefin polymers and EU Regulation 10/2011 as applicable. Compliance is not inherent to the resin; it depends on additive package, colorants, conversion conditions, and intended food-contact time and temperature. The current supplier safety data sheet and product datasheet should be consulted for REACH and RoHS status.

    The resin should be stored in a dry, shaded area at ambient temperature. Prolonged exposure to direct sunlight or ultraviolet radiation can cause surface oxidation and reduce impact strength. Processing with regrind is possible, but the proportion should be controlled and validated on the specific mold because repeated heat histories lower molecular weight and narrow the processing window.

    Top